EP1825553B1 - Electrically conductive fuel cell contact materials - Google Patents

Electrically conductive fuel cell contact materials Download PDF

Info

Publication number
EP1825553B1
EP1825553B1 EP05803472.9A EP05803472A EP1825553B1 EP 1825553 B1 EP1825553 B1 EP 1825553B1 EP 05803472 A EP05803472 A EP 05803472A EP 1825553 B1 EP1825553 B1 EP 1825553B1
Authority
EP
European Patent Office
Prior art keywords
particles
layer
coarse
fuel cell
fine
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
EP05803472.9A
Other languages
German (de)
English (en)
French (fr)
Other versions
EP1825553A4 (en
EP1825553A1 (en
Inventor
Anthony Wood
Zheng Tang
Tahir Joia
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Versa Power Systems Ltd
Original Assignee
Versa Power Systems Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Versa Power Systems Ltd filed Critical Versa Power Systems Ltd
Publication of EP1825553A1 publication Critical patent/EP1825553A1/en
Publication of EP1825553A4 publication Critical patent/EP1825553A4/en
Application granted granted Critical
Publication of EP1825553B1 publication Critical patent/EP1825553B1/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/02—Details
    • H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/0204—Non-porous and characterised by the material
    • H01M8/0215—Glass; Ceramic materials
    • H01M8/0217—Complex oxides, optionally doped, of the type AMO3, A being an alkaline earth metal or rare earth metal and M being a metal, e.g. perovskites
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/90—Selection of catalytic material
    • H01M4/9016—Oxides, hydroxides or oxygenated metallic salts
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/02—Details
    • H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/023—Porous and characterised by the material
    • H01M8/0241—Composites
    • H01M8/0245—Composites in the form of layered or coated products
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/10—Fuel cells with solid electrolytes
    • H01M8/12—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte
    • H01M2008/1293—Fuel cells with solid oxide electrolytes
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30—Hydrogen technology
    • Y02E60/50—Fuel cells
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T29/00—Metal working
    • Y10T29/43—Electric condenser making

Definitions

  • the present invention relates to a multilayer design of contact materials which may include electrically conductive perovskites.
  • High temperature fuel cells like solid oxide fuel cells comprise an electrolyte sandwiched between a cathode and an anode.
  • Oxygen combines with electrons at the cathode to form oxygen ions, which are conducted through the ion-conducting ceramic electrolyte to the anode.
  • oxygen ions combine with hydrogen and carbon monoxide to form water and carbon dioxide thereby liberating electrons.
  • the fuel cells are stacked and interleaved with interconnect plates which distribute gases to the electrode surfaces and which act as current collectors.
  • Contact pastes are used to bond the electrode to an interconnect and must therefore be electrically conductive.
  • U.S. Patent No. 6,420,064 a cathode contact layer comprised of lanthanum cobaltate is disclosed.
  • German Patent No. DE 19627504 discloses a connection lead plate for a high temperature fuel stack having at least part of its surface coated with a contact layer comprising a lower oxidic layer, a middle ceramic layer, and an upper ceramic layer having less porosity than the upper ceramic layer.
  • Lanthanum cobaltate also known as lanthanum cobaltite, is a perovskite, which is a well-known class of mineral oxides characterized by a cubic or orthorhombic crystalline structure.
  • Perovskites may be described by the formula ABO 3 , where A represents divalent and/or trivalent ions and B represents trivalent and/or tetravalent ions, while the O atom is the oxygen ion.
  • the divalent, trivalent and tetravalent ions may include La 3+ , Sm 3+ , Sr 2+ , Ca 2+ , Co 3+ , Ni 3+ , ,Fe 3+ , Cr 3+ , Mn 3+ or Mn 4+ amongst others.
  • this ABO 3 structure in a general sense can be thought of as face centered cubic (FCC) lattice with A atoms at the corners and the O atoms on the faces.
  • the B atom is located at the center of the lattice.
  • LC Some perovskites such as LC are reasonably good electrical conductors.
  • LC suffers from one significant disadvantage. If sintered, its coefficient of thermal expansion is significantly greater than that of the bulk cell. Consequently, thermal cycling of the fuel cell results in large thermal stresses and the contact paste may break away from the cell and interconnect resulting in poor electrical contact.
  • contact paste materials which display better interface performance with the cell can have poor interface performance with the interconnect.
  • the present invention provides for a contact material comprising stress relief means for use in fuel cell stack between a fuel cell electrode and an interconnect.
  • the contact material is electrically conductive and porous to permit the flow of reactant to the electrode.
  • the electrode is a cathode.
  • the invention comprises a fuel cell stack comprising:
  • the stress relief layer may additionally comprise a separately formed layer of a conductive ceramic material which is pressed against the pore forming material. That separately formed layer may itself include particles of a pore forming material.
  • the pore forming material combusts, leaving a void space. If the pore forming material was introduced in particular form, the stress relief layer will be more porous and structurally weaker. If the pore forming material was introduced in a layer, a fracture plane will be left. Alternatively, a fracture plane may be introduced by forming two halves of a stress relief layer and contacting them without binding or otherwise linking them together.
  • the invention may comprise a method of forming a stress relief layer in a contact layer disposed between at least one electrode of a fuel cell and an adjacent interconnect, the contact layer comprising at least two outer layers and a central layer of electrically conductive material, wherein one of the outer layers adheres to the at least one electrode and the other outer layer adheres to the interconnect, wherein the central layer comprises the stress relief layer, said method comprising the steps of: forming the stress relief layer from:
  • the present invention provides for a perovskite contact material which may be used to interface between a solid oxide fuel cell electrode and an interconnect or a current collector.
  • a perovskite contact material which may be used to interface between a solid oxide fuel cell electrode and an interconnect or a current collector.
  • a portion of a fuel cell stack is illustrated as an exploded view in Figure 1 and in cross-section in Figure 2 .
  • a single fuel cell (10) consists of an anode (12) supported structure having a thin electrolyte (14) and cathode (16) layer.
  • a single fuel cell unit also includes an interconnect (18) which may be a monolithic plate having flow-directing ribs (20) stamped as shown in Figure 1 .
  • the ribs (20) assist in providing an even distribution of air flow across the entire surface of the cathode between the air intake and exhaust manifolds.
  • the cathode may comprise a composite material comprising a noble metal such as palladium and a ceramic such as yttrium stabilized zirconium, as described in co-owned U.S. Patent No. 6,420 ,064 .
  • the contact material (22) of the present invention is applied to one or both of the cathode and interconnect faces upon assembly of the fuel cell stack.
  • the contact material may be applied by screen printing, as is well known in the art.
  • a layer may be screen printed onto the cathode surface and allowed to dry.
  • the contact material paste dries as a porous green ceramic layer and may then be sintered prior to assembly of fuel cell units in the stack. Alternatively, the material may not be sintered before stack assembly, in which case, the contact material is sintered during operation of the fuel cell.
  • a second contact layer is then applied (the fracture layer) and dried.
  • a thin layer of the contact material as a wet paste is screen printed onto the cell dried layer(s) or the interconnect surface and the interconnect is then contacted with the cathode surface. If the interconnect is corrugated or ribbed, the contact material may or may not fill in the void areas of the interconnect. The contact material must be porous to allow reactants to flow from the interconnect and reach the fuel cell electrode.
  • Perovskites of the present invention may be described by the general formula ABO 3 , where A is a doped or undoped rare earth metal, lanthanide or mixed lanthanide, and B is a doped or undoped transition metal, where the perovskite has a coefficient of thermal expansion (CTE) which closely matches that of the fuel cell electrode or the interconnect.
  • CTE coefficient of thermal expansion
  • a CTE is considered to closely match another CTE if it is within about 5 x 10 -6 K -1 of the other CTE.
  • the coefficient of thermal expansion of a material may be determined empirically or by estimation using known and published values. Whether or not two materials have closely matched coefficients of expansion may also be determined experimentally by thermal cycling the two materials adhered to each other and observing the loss of adhesion.
  • a contact material of the present invention may be applied to an interconnect or to a fuel cell electrode, and the two materials thermally cycled within the operating temperature range of a solid oxide fuel cell. If no, or substantially none, loss of adhesion is observed, then a person skilled in the art may conclude that the CTE's of the two materials are likely to be closely matched.
  • the transition metal may comprise cobalt, nickel, iron, copper, zinc or lead.
  • B comprises cobalt doped with nickel as follows: Co 1-y Ni y where 0.3 ⁇ y ⁇ 0.7.
  • y is about 0.4.
  • Nickel is a preferred material because the inclusion of nickel in the B-site tends to lower the coefficient of thermal expansion.
  • the perovskite formed with nickel is highly electrically conductive but is not very reactive with other materials.
  • the A element is preferably lanthanum and may be doped with an alkaline earth metal such as strontium, barium or calcium to improve electrical conductivity. Therefore, A may comprise La 1-x E x wherein E is an alkaline earth metal and 0.0 ⁇ x ⁇ 0.8. Lanthanum cobalt nickel oxide materials are referred to herein as "LCN".
  • a particularly preferred LCN material is La 1-x E x Co 0.6 Ni 0.4 where x is greater than or equal to zero and less than about 0.7. Preferably, x is less than 0.5.
  • the A and B elements may be stoichiometric or non-stoichiometric. If non-stoichiometric, the A:B ratio may vary from about 0.9 to about 1.1.
  • the perovskites of the present invention may be applied as a paste using well-known solvents and binders to either or both of the cathode and interconnect in a fuel cell unit and sintered prior to assembly of the fuel cell stack.
  • the paste may be unsintered prior to assembly of the fuel cell stack and sintered in situ upon operation of the fuel cell stack.
  • Stack operating temperatures may reach about 800° C.
  • Sintering additives to lower the sintering temperature of the perovskite may be desirable or necessary. Suitable sintering additives or aids such as copper, silver, glass frit or tin are well-known in the art.
  • a contact material of the present invention may also be used in the interface between the anode surface and an interconnect and its use is not restricted to the cathode surface.
  • the contact paste material is applied in a multilayer configuration which may provide better resistance to thermal cycling degradation and long term degradation.
  • the contact paste is applied in three layers in which the outer contact layers adhere to the fuel cell electrode and interconnect respectively, and the central layer comprises a stress relief layer.
  • the outer contact layers comprise fine conductive particles while the stress relief layer comprises coarse conductive particles.
  • the conductive particles in either or both the fine and coarse layers preferably comprise conductive perovskites, including those perovskites described herein, or perovskites having a K 2 NiF 4 -type structure (e.g. La 2 Ni 1-x Co x O 4 ) or any other electrically conducting ceramic powder compatible with the fuel cell electrolyte and electrode materials.
  • fine particles comprise particles having diameters less than about 2 ⁇ m and preferably about 0.3 to about 1.1 ⁇ m.
  • coarse particles comprises particles that are at least one and a half times the particle diameter of the fine particles, and preferably greater than about twice the diameter of the fine particles.
  • coarse particles Preferably, coarse particles have diameters greater than about 1 ⁇ m and more preferably greater than about 1.5 ⁇ m.
  • the stress relief layer may be formed of a conductive ceramic material, such as the perovskites described herein, which has similar chemistry and similar sintering characteristics to the fine outer layers, but which comprises coarse particles.
  • the stress relief layer may be formed from a conductive ceramic material which has significantly different sintering characteristics than the fine layers.
  • the stress relief layer may be formed of lanthanum strontium manganite (LSM), which has a significantly higher sintering temperature than LC or LCN.
  • LSM lanthanum strontium manganite
  • the stress relief particle size may be fine or coarse.
  • the stress relief layer would not sinter or sinter to the same extent as the other layers.
  • the stress relief layer may be formed of a porous metallic material such as expanded metal, or a fine metal mesh.
  • the stress relief layer may be porous or highly porous.
  • the stress relief layer comprises coarse particles and has a porosity of between about 25% to about 70%.
  • the stress relief layer may be about 30% to about 50% porous.
  • Porous metallic stress relief layers may be more porous, up to about 95%.
  • the fine particle layers may be thinner or thicker than the coarse central layer.
  • the fine particle layers are less than about 25 ⁇ m thick while the coarse central layer may be about 10 ⁇ m to about 50 ⁇ m thick.
  • the combined thickness of the multilayer contact materials may be about 60 to 120 ⁇ m, depending on the stack design and seal thicknesses. The combined thickness should preferably not exceed 200 ⁇ m.
  • the layers may be applied by screen printing a paste and sintered prior to stack assembly or left unsintered as described above.
  • Sintering aids may be included if necessary or desired. The necessity or desirability of a sintering aid may be determined empirically by one skilled in the art.
  • a layer of fine lanthanum cobalt nickel oxide (LCN) particles is applied to the fuel cell electrode surface by screen printing.
  • the LCN particles have an average particle size of about 1.0 ⁇ m with about 50% of the particles falling in the range of about 0.5 ⁇ m to about 1.1 ⁇ m.
  • This layer of fine LCN particles may be less than about 25 ⁇ m thick and may or may not be sintered.
  • a layer of coarse LCN material is applied by screen printing onto the first fine layer and allowed to dry.
  • the coarse LCN particles have an average particle size of between about 2 to about 3 ⁇ m, with a majority of the particles falling in the range between about 1 ⁇ m to about 10 ⁇ m.
  • the remaining fine layer of LCN is screen printed onto this layer on the cell or the interconnect just prior to assembly of the stack.
  • LC may be used in place of LCN in any or all of the layers.
  • the multilayered approach may provide better long term stability by providing a sacrificial fracture layer which absorbs expansion mismatches during thermal cycling and long term operation.
  • the interfaces between the fine layers and the fuel cell and interconnect respectively remain intact while physical stresses are absorbed by the central stress relief layer.
  • a scanning electron micrograph demonstrates such a fracture in an autopsied fuel cell. The inventors have found that electrical conductivity through the contact material is maintained while the layers are compressed in a stack despite such horizontal fractures in the stress relief layer.
  • the fracturing of the stress relief layer, or the interface between the stress relief layer and a fine outer layer may be facilitated by the addition of pore forming material or a fracture layer. This may be desirable or necessary if the cathode contact material is not pre-fired.
  • a pore former may be added to the stress relief layer which will have the effect of weakening the stress relief layer internally, facilitating the formation of fractures.
  • Pore formers may comprise organic particulate matter and may include graphite, corn starch or polystyrene, or other materials which combust at or about 500° C. The pore former burns out before reaching the operating temperature of the fuel cell, or during a pre-sintering process, introducing voids in the structure of the stress relief layer.
  • the pore forming particles may preferably be about 1 ⁇ m to about 50 ⁇ m in size, and more preferably less than about 20 ⁇ m.
  • the pore forming particles may be added to the coarse particle composition which is screen printed or otherwise applied to a fine particle layer. Sufficient pore forming material may be added to a level of about 20 to about 60 % by volume. With the addition of the pore former, the stress relief layer may be about 30-70% porous, preferably greater than about 50% porous, after combustion of the pore forming material. With larger pore forming particle sizes, the void spaces would of course be larger, but fewer in number.
  • a weakened area may be introduced to the contact material by adding a fracture layer between the stress relief layer and the fine particle outer layer, or within the stress relief layer itself.
  • the fracture layer may be added, for example, by adding a thin layer of an organic substance, which may the same as the pore forming substances described above. Suitable fracture layers may therefore comprise graphite, corn starch or polystyrene. Again, prior to reaching the operating temperature of the cell, or during a pre-sintering process, the fracture layer will burn out, leaving a weakened fracture plane.
  • the fracture layer may be applied by spraying a suspension of the particles or by screen printing. Preferably, the fracture layer may be about 1-20 ⁇ m thick.
  • a pre-fractured stress relief layer may be provided.
  • a fine layer and a coarse stress relief layer may be applied to each of the cathode and the interconnect and allowed to dry.
  • the coarse layer may or may not include pore formers as described above.
  • the respective stress relief layers are pressed together.
  • the boundary between the two coarse stress relief layers forms a fracture plane, creating what is in effect a single pre-fractured stress relief layer.
  • the two coarse stress relief layers may include pore forming particles as described above.
  • a pre-fractured stress layer may be formed by pressing together a fracture layer formed from a layer of a pore forming material as described above and a coarse layer.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Electrochemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Sustainable Development (AREA)
  • Manufacturing & Machinery (AREA)
  • Sustainable Energy (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Materials Engineering (AREA)
  • Ceramic Engineering (AREA)
  • Composite Materials (AREA)
  • Fuel Cell (AREA)
  • Inert Electrodes (AREA)
EP05803472.9A 2004-11-16 2005-11-04 Electrically conductive fuel cell contact materials Active EP1825553B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US10/904,563 US7190568B2 (en) 2004-11-16 2004-11-16 Electrically conductive fuel cell contact materials
PCT/CA2005/001695 WO2006053422A1 (en) 2004-11-16 2005-11-04 Electrically conductive fuel cell contact materials

Publications (3)

Publication Number Publication Date
EP1825553A1 EP1825553A1 (en) 2007-08-29
EP1825553A4 EP1825553A4 (en) 2012-01-11
EP1825553B1 true EP1825553B1 (en) 2018-12-26

Family

ID=36386022

Family Applications (1)

Application Number Title Priority Date Filing Date
EP05803472.9A Active EP1825553B1 (en) 2004-11-16 2005-11-04 Electrically conductive fuel cell contact materials

Country Status (7)

Country Link
US (1) US7190568B2 (ja)
EP (1) EP1825553B1 (ja)
JP (1) JP5279272B2 (ja)
AU (1) AU2005306525B2 (ja)
CA (1) CA2588025C (ja)
DK (1) DK1825553T3 (ja)
WO (1) WO2006053422A1 (ja)

Families Citing this family (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7892698B2 (en) * 2003-07-18 2011-02-22 Versa Power Systems, Ltd. Electrically conductive fuel cell contact material
EP1850412A1 (en) * 2006-04-26 2007-10-31 Technical University of Denmark A multi-layer coating
GB0715225D0 (en) 2007-08-03 2007-09-12 Rolls Royce Fuel Cell Systems A fuel cell and a method of manufacturing a fuel cell
GB0715218D0 (en) 2007-08-03 2007-09-12 Rolls Royce Fuel Cell Systems A fuel cell and a method of manufacturing a fuel cell
FR2935843B1 (fr) * 2008-09-11 2011-02-11 Commissariat Energie Atomique Electrolyte pour pile sofc et son procede de fabrication.
CN102217130A (zh) * 2008-11-21 2011-10-12 博隆能源股份有限公司 用于生产燃料电池组件的涂覆工艺
JP5388833B2 (ja) * 2009-12-24 2014-01-15 京セラ株式会社 セルスタックおよびそれを具備する燃料電池モジュールならびに燃料電池装置
KR101300157B1 (ko) 2009-12-28 2013-08-26 주식회사 포스코 고체 산화물 연료 전지용 복합 세라믹 접촉재 및 그 제조방법
WO2012040253A1 (en) 2010-09-20 2012-03-29 Nextech Materials, Ltd. Fuel cell repeat unit and fuel cell stack
WO2012142537A1 (en) * 2011-04-13 2012-10-18 Nextech Materials Ltd. Protective coatings for metal alloys and methods incorporating the same
US9993874B2 (en) 2014-02-25 2018-06-12 Bloom Energy Corporation Composition and processing of metallic interconnects for SOFC stacks
US9559366B2 (en) 2014-03-20 2017-01-31 Versa Power Systems Ltd. Systems and methods for preventing chromium contamination of solid oxide fuel cells
US10084192B2 (en) 2014-03-20 2018-09-25 Versa Power Systems, Ltd Cathode contact layer design for preventing chromium contamination of solid oxide fuel cells

Family Cites Families (37)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3766442A (en) * 1972-02-04 1973-10-16 Mallory & Co Inc P R Electrical component terminal
US4136382A (en) * 1978-01-18 1979-01-23 Exxon Research & Engineering Co. Converter system
DE2837118C2 (de) * 1978-08-25 1982-05-19 Dornier System Gmbh, 7990 Friedrichshafen Poröse Oxidelektroden für elektrochemische Hochtemperaturzellen
DE3246706A1 (de) * 1982-12-17 1984-06-20 Danfoss As Stromversorgungsvorrichtung fuer einen wechselstromverbraucher
DE3307623C2 (de) * 1983-03-04 1986-06-05 Lenze GmbH & Co KG Aerzen, 3258 Aerzen Verfahren und Schaltungsanordnung zur Regelung eines Wechselstrom- oder Drehstrommotors
US4883497A (en) * 1988-03-28 1989-11-28 Arch Development Corporation Formation of thin walled ceramic solid oxide fuel cells
JPH038264A (ja) * 1989-06-05 1991-01-16 Sanyo Electric Co Ltd 固体電解質燃料電池
EP0432381A1 (de) * 1989-10-12 1991-06-19 Asea Brown Boveri Ag Bauteilanordnung zur Stromführung für keramische Hochtemperatur-Brennstoffzellen
US5132352A (en) * 1990-04-27 1992-07-21 Westinghouse Electric Corp. Tape method of forming a thin layer of doped lanthanum chromite particles and of bonding such on an electrode
US4988582A (en) * 1990-05-04 1991-01-29 Bell Communications Research, Inc. Compact fuel cell and continuous process for making the cell
US5136216A (en) * 1991-02-15 1992-08-04 York International Corporation Ac motor drive system
US5218283A (en) * 1991-02-15 1993-06-08 York International Corporation AC motor drive system with a two phase power supply
US5146147A (en) * 1991-02-28 1992-09-08 York International Corporation Ac motor drive system
US5315497A (en) * 1991-11-07 1994-05-24 Premier Power, Inc. Symmetrical universal AC-AC power conditioner
JPH0685173A (ja) * 1992-07-17 1994-03-25 Toshiba Corp 半導体集積回路用キャパシタ
US5339348A (en) * 1992-11-02 1994-08-16 General Electric Company X-ray tube rotor controller using the main high voltage inverters for acceleration
DE4237602A1 (de) * 1992-11-06 1994-05-11 Siemens Ag Hochtemperatur-Brennstoffzellen-Stapel und Verfahren zu seiner Herstellung
US5356730A (en) * 1993-03-26 1994-10-18 Alliedsignal Inc. Monolithic fuel cell having improved interconnect layer
US5406185A (en) * 1993-06-04 1995-04-11 Strunk; Timothy L. Two-phase inverter drive for a three-phase motor
JP3153408B2 (ja) * 1994-03-10 2001-04-09 株式会社日立製作所 直列多重電力変換器
JP3687861B2 (ja) * 1995-03-20 2005-08-24 株式会社ルネサステクノロジ 制御システム及び相補ノンオーバーラップｐｗｍ信号を形成する方法
US5656387A (en) * 1995-10-10 1997-08-12 Northwestern University Solid-oxide fuel cells having nickel and yttria-stabilized zirconia anodes and method of manufacture
DE19609133C1 (de) * 1996-03-08 1997-09-04 Siemens Ag Bipolare Platte für einen Hochtemperatur-Brennstoffzellenstapel und deren Verwendung
DE19627504C1 (de) * 1996-07-08 1997-10-23 Siemens Ag Verbundleiterplatte und Verwendung einer Verbundleiterplatte für einen Hochtemperatur-Brennstoffzellenstapel
JPH1092446A (ja) * 1996-09-13 1998-04-10 Fuji Electric Corp Res & Dev Ltd 固体電解質型燃料電池
WO1998043308A1 (de) * 1997-03-20 1998-10-01 Siemens Aktiengesellschaft Hochtemperatur-brennstoffzelle mit verbundstoff-kathode
JP2000053424A (ja) * 1998-07-24 2000-02-22 Sulzer Hexis Ag インタ―コネクタのコ―ティングのためのペロブスカイト、インタ―コネクタ及び燃料セル電池
DE19835253A1 (de) * 1998-08-04 2000-01-13 Siemens Ag Verfahren zur Herstellung einer Hochtemperatur-Brennstoffzelle
CA2378384A1 (en) * 1999-07-09 2001-01-18 Siemens Aktiengesellschaft Electrical bonding protected against oxidation on the gas combustion side of a high temperature fuel cell
CA2352391C (en) 1999-10-08 2009-08-25 Global Thermoelectric Inc. Composite electrodes for solid state electrochemical devices
JP2002358980A (ja) * 2001-05-30 2002-12-13 Mitsubishi Materials Corp 固体電解質型燃料電池
TW559845B (en) * 2001-07-30 2003-11-01 Matsushita Electric Ind Co Ltd Solid electrolytic capacitor and its manufacturing method
EP1328030A1 (en) * 2002-01-15 2003-07-16 N.V. Bekaert S.A. Metal stack for fuel cells or electrolysers
NL1020985C2 (nl) * 2002-07-03 2004-01-06 Stichting Energie Anodegedragen brandstofcel.
JP2004087892A (ja) * 2002-08-28 2004-03-18 Matsushita Electric Ind Co Ltd アルミ電解コンデンサ及びその製造方法
JP4472277B2 (ja) * 2003-04-10 2010-06-02 Ｎｅｃトーキン株式会社 チップ型固体電解コンデンサ
CA2530205C (en) * 2003-07-18 2011-10-18 Xinge Zhang Electrically conductive fuel cell contact material

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
None *

Also Published As

Publication number Publication date
EP1825553A4 (en) 2012-01-11
JP2008521179A (ja) 2008-06-19
JP5279272B2 (ja) 2013-09-04
US7190568B2 (en) 2007-03-13
US20060104008A1 (en) 2006-05-18
DK1825553T3 (en) 2019-02-18
AU2005306525B2 (en) 2010-07-15
CA2588025C (en) 2013-07-30
CA2588025A1 (en) 2006-05-26
EP1825553A1 (en) 2007-08-29
WO2006053422A1 (en) 2006-05-26
AU2005306525A1 (en) 2006-05-26

Similar Documents

Publication Publication Date Title
US8962218B2 (en) Electrically conductive fuel cell contact material
KR101083701B1 (ko) 가역 고형 산화물 연료전지 스택 및 이의 제조방법
KR101045168B1 (ko) 완전하게 밀봉되고 지지된 세라믹 막, 및 이를 포함하는전기화학 전지 및 전기화학 전지 적층체
KR101175599B1 (ko) 인터커넥터용 재료, 셀간 분리 구조체 및 고체 전해질형 연료 전지
JP5469135B2 (ja) 燃料電池スタック
KR101162806B1 (ko) 자가-지지형 세라믹 멤브레인 및 전기화학 전지 및 이것을포함하는 전기화학 전지 적층체
JP3502012B2 (ja) 固体電解質型燃料電池、およびその製造方法
JP4517466B2 (ja) 固体酸化物型燃料電池
EP1825553B1 (en) Electrically conductive fuel cell contact materials
WO2013012009A1 (ja) 固体酸化物形燃料電池用電気的接続材、固体酸化物形燃料電池、固体酸化物形燃料電池モジュール及び固体酸化物形燃料電池の製造方法
US20120037499A1 (en) Composite oxygen electrode and method for preparing same
WO2012144119A1 (ja) 燃料電池セル及び燃料電池
WO2011138915A1 (ja) 高温構造材料、固体電解質形燃料電池用構造体および固体電解質形燃料電池
JPH10172590A (ja) 固体電解質型燃料電池
EP3211703B1 (en) Fuel cell
JP2005085522A (ja) 支持膜式固体酸化物形燃料電池
JP2005322452A (ja) 固体酸化物形燃料電池用セル板及び固体酸化物形燃料電池
CA2560769C (en) Electrolyte electrode assembly and method of producing the same

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 20070614

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LI LT LU LV MC NL PL PT RO SE SI SK TR

DAX Request for extension of the european patent (deleted)
A4 Supplementary search report drawn up and despatched

Effective date: 20111213

RIC1 Information provided on ipc code assigned before grant

Ipc: H01M 8/10 20060101ALI20111207BHEP

Ipc: H01M 4/90 20060101ALI20111207BHEP

Ipc: H01M 8/24 20060101AFI20111207BHEP

Ipc: H01M 8/02 20060101ALI20111207BHEP

Ipc: H01M 4/86 20060101ALI20111207BHEP

17Q First examination report despatched

Effective date: 20130529

REG Reference to a national code

Ref country code: DE

Ref legal event code: R079

Ref document number: 602005055201

Country of ref document: DE

Free format text: PREVIOUS MAIN CLASS: H01M0008240000

Ipc: H01M0008021700

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: GRANT OF PATENT IS INTENDED

RIC1 Information provided on ipc code assigned before grant

Ipc: H01M 8/0217 20160101AFI20170519BHEP

Ipc: H01M 4/90 20060101ALI20170519BHEP

Ipc: H01M 8/124 20160101ALI20170519BHEP

Ipc: H01M 8/0245 20160101ALI20170519BHEP

INTG Intention to grant announced

Effective date: 20170626

GRAJ Information related to disapproval of communication of intention to grant by the applicant or resumption of examination proceedings by the epo deleted

Free format text: ORIGINAL CODE: EPIDOSDIGR1

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: EXAMINATION IS IN PROGRESS

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: GRANT OF PATENT IS INTENDED

INTC Intention to grant announced (deleted)
INTG Intention to grant announced

Effective date: 20171207

GRAJ Information related to disapproval of communication of intention to grant by the applicant or resumption of examination proceedings by the epo deleted

Free format text: ORIGINAL CODE: EPIDOSDIGR1

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

INTG Intention to grant announced

Effective date: 20180612

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE PATENT HAS BEEN GRANTED

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LI LT LU LV MC NL PL PT RO SE SI SK TR

REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

REG Reference to a national code

Ref country code: CH

Ref legal event code: EP

RIC2 Information provided on ipc code assigned after grant

Ipc: H01M 8/124 20160101ALI20170519BHEP

Ipc: H01M 4/90 20060101ALI20170519BHEP

Ipc: H01M 8/0217 20160101AFI20170519BHEP

Ipc: H01M 8/0245 20160101ALI20170519BHEP

REG Reference to a national code

Ref country code: DE

Ref legal event code: R096

Ref document number: 602005055201

Country of ref document: DE

REG Reference to a national code

Ref country code: AT

Ref legal event code: REF

Ref document number: 1082679

Country of ref document: AT

Kind code of ref document: T

Effective date: 20190115

REG Reference to a national code

Ref country code: IE

Ref legal event code: FG4D

REG Reference to a national code

Ref country code: CH

Ref legal event code: PK

Free format text: BERICHTIGUNGEN

RIC2 Information provided on ipc code assigned after grant

Ipc: H01M 8/0245 20160101ALI20170519BHEP

Ipc: H01M 8/124 20160101ALI20170519BHEP

Ipc: H01M 8/0217 20160101AFI20170519BHEP

Ipc: H01M 4/90 20060101ALI20170519BHEP

REG Reference to a national code

Ref country code: DK

Ref legal event code: T3

Effective date: 20190212

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LV

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20181226

Ref country code: LT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20181226

Ref country code: BG

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190326

REG Reference to a national code

Ref country code: NL

Ref legal event code: MP

Effective date: 20181226

REG Reference to a national code

Ref country code: LT

Ref legal event code: MG4D

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190327

Ref country code: SE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20181226

REG Reference to a national code

Ref country code: AT

Ref legal event code: MK05

Ref document number: 1082679

Country of ref document: AT

Kind code of ref document: T

Effective date: 20181226

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20181226

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: ES

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20181226

Ref country code: PT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190426

Ref country code: CZ

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20181226

Ref country code: PL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20181226

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20181226

Ref country code: EE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20181226

Ref country code: IS

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190426

Ref country code: RO

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20181226

REG Reference to a national code

Ref country code: DE

Ref legal event code: R097

Ref document number: 602005055201

Country of ref document: DE

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: AT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20181226

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

26N No opposition filed

Effective date: 20190927

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20181226

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: TR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20181226

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LI

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20191130

Ref country code: CH

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20191130

Ref country code: MC

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20181226

Ref country code: LU

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20191104

REG Reference to a national code

Ref country code: BE

Ref legal event code: MM

Effective date: 20191130

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20191130

Ref country code: IE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20191104

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: BE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20191130

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: CY

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20181226

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: HU

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT; INVALID AB INITIO

Effective date: 20051104

P01 Opt-out of the competence of the unified patent court (upc) registered

Effective date: 20230516

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: IT

Payment date: 20231010

Year of fee payment: 19

Ref country code: FI

Payment date: 20231116

Year of fee payment: 19

Ref country code: DE

Payment date: 20230912

Year of fee payment: 19

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DK

Payment date: 20240105

Year of fee payment: 19

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 20240912

Year of fee payment: 20